Removal of hydroquinone from water by electrocoagulation using flow cell and optimization by response surface methodology

被引:30
作者
Prabhakaran, D. [2 ]
Basha, C. A. [1 ]
Kannadasan, T. [3 ]
Aravinthan, P. [4 ]
机构
[1] CSIR, Cent Electrochem Res Inst, Karaikkudi 630006, Tamil Nadu, India
[2] Coimbatore Inst Technol, Coimbatore, Tamil Nadu, India
[3] Anna Univ Coimbatore, Res Ctr, Coimbatore, Tamil Nadu, India
[4] Covanta Samalpatti Operating Private Ltd, Safety Hlth & Environm Dept, Parandapalli Village, India
来源
JOURNAL OF ENVIRONMENTAL SCIENCE AND HEALTH PART A-TOXIC/HAZARDOUS SUBSTANCES & ENVIRONMENTAL ENGINEERING | 2010年 / 45卷 / 04期
关键词
Hydroquinone; electrocoagulation; mono and bipolar flow cell; response surface method; TEXTILE WASTE-WATER; PHOTOCATALYTIC DEGRADATION; COAGULATION; SEPARATION; EFFLUENTS; CU2+;
D O I
10.1080/10934520903540174
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In this study, hydroquinone was removed from water by electrocoagulation using flow electrolyzer in mono polar and bipolar configurations in a batch recirculation mode of operation. Treatment performances of such effluents have been evaluated in terms of chemical oxygen demand removal. The effect of important operating parameters such as current density, flow rate, concentration of hydroquinone and supporting electrolyte on the pollutant removal and energy consumption is critically evaluated. The experimental data were analyzed using response surface methodology (RSM). Maximum COD removal in monopolar configuration of 80.95% was noticed at condition of supporting electrolyte concentration 2.67 g L-1, flow rate 27 mL min(-1), current density 0.7 A dm(-2) at energy consumption of 2.36 kWh per kg of COD for the 1000 mg L-1 of hydroquinone concentration. In the case of bipolar configuration a maximum COD removal of 87.13 was noticed at: supporting electrolyte concentration 4 g L-1, flow rate 29.15 mL min(-1), current density 1 Adm(-2) at energy consumption of 8.495 kWh per kg of COD for the same hydroquinone concentration.
引用
收藏
页码:400 / 412
页数:13
相关论文
共 29 条
[1]   Treatment of electroplating wastewater containing Cu2+, Zn2+ and Cr(VI) by electrocoagulation [J].
Adhoum, N ;
Monser, L ;
Bellakhal, N ;
Belgaied, JE .
JOURNAL OF HAZARDOUS MATERIALS, 2004, 112 (03) :207-213
[2]   Ozonation of high strength segregated effluents from a woollen textile dyeing and finishing plant [J].
Baban, A ;
Yediler, A ;
Lienert, D ;
Kemerdere, N ;
Kettrup, A .
DYES AND PIGMENTS, 2003, 58 (02) :93-98
[3]   REMOVAL OF PHENOLIC-COMPOUNDS FROM WASTE-WATER USING MUTANT STRAIN OF PSEUDOMONAS-PICTORUM [J].
CHITRA, S ;
SEKARAN, G ;
PADMAVATHI, S ;
CHANDRAKASAN, G .
JOURNAL OF GENERAL AND APPLIED MICROBIOLOGY, 1995, 41 (03) :229-237
[4]  
Clesceri L, 1998, STANDARD METHODS EXA
[5]   A sensitive flow analysis system for the fluorimetric determination of low levels of formaldehyde in alcoholic beverages [J].
de Oliveira, Fabio Santos ;
Sousa, Eliane Teixeira ;
de Andrade, Jailson B. .
TALANTA, 2007, 73 (03) :561-566
[6]   Removal of chromium(VI) from wastewater by combined electrocoagulation-electroflotation without a filter [J].
Gao, P ;
Chen, XM ;
Shen, F ;
Chen, GH .
SEPARATION AND PURIFICATION TECHNOLOGY, 2005, 43 (02) :117-123
[7]   Application of response surface methodology for predicting weld bead quality in submerged are welding of pipes [J].
Gunaraj, V ;
Murugan, N .
JOURNAL OF MATERIALS PROCESSING TECHNOLOGY, 1999, 88 (1-3) :266-275
[8]   Deciphering the science behind electrocoagulation to remove suspended clay particles from water [J].
Holt, PK ;
Barton, GW ;
Mitchell, CA .
WATER SCIENCE AND TECHNOLOGY, 2004, 50 (12) :177-184
[9]   Electrochemical treatment of heavy metals (Cu2+, Cr6+Ni2+) from industrial effluent and modeling of copper reduction [J].
Hunsom, M ;
Pruksathorn, K ;
Damronglerd, S ;
Vergnes, H ;
Duverneuil, P .
WATER RESEARCH, 2005, 39 (04) :610-616
[10]  
*INT PROGR CHEM SA, 1994, HYDR ENV HLTH CRIT 1